US910858A - Production of hydrazin. - Google Patents
Production of hydrazin. Download PDFInfo
- Publication number
- US910858A US910858A US40000207A US1907400002A US910858A US 910858 A US910858 A US 910858A US 40000207 A US40000207 A US 40000207A US 1907400002 A US1907400002 A US 1907400002A US 910858 A US910858 A US 910858A
- Authority
- US
- United States
- Prior art keywords
- hydrazin
- ammonia
- monochloramin
- excess
- production
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 title description 17
- 238000004519 manufacturing process Methods 0.000 title description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 34
- 229910021529 ammonia Inorganic materials 0.000 description 17
- QDHHCQZDFGDHMP-UHFFFAOYSA-N Chloramine Chemical compound ClN QDHHCQZDFGDHMP-UHFFFAOYSA-N 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 9
- 239000000203 mixture Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000009835 boiling Methods 0.000 description 5
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical class Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 5
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000003292 glue Substances 0.000 description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 3
- 239000005708 Sodium hypochlorite Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- ZGCHATBSUIJLRL-UHFFFAOYSA-N hydrazine sulfate Chemical compound NN.OS(O)(=O)=O ZGCHATBSUIJLRL-UHFFFAOYSA-N 0.000 description 2
- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 244000299461 Theobroma cacao Species 0.000 description 1
- 235000005764 Theobroma cacao ssp. cacao Nutrition 0.000 description 1
- 235000005767 Theobroma cacao ssp. sphaerocarpum Nutrition 0.000 description 1
- -1 albumen Polymers 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 235000001046 cacaotero Nutrition 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- SURLGNKAQXKNSP-DBLYXWCISA-N chlorin Chemical compound C\1=C/2\N/C(=C\C3=N/C(=C\C=4NC(/C=C\5/C=CC/1=N/5)=CC=4)/C=C3)/CC\2 SURLGNKAQXKNSP-DBLYXWCISA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008098 formaldehyde solution Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 239000000341 volatile oil Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/082—Compounds containing nitrogen and non-metals and optionally metals
- C01B21/16—Hydrazine; Salts thereof
Definitions
- the first reaction resulting in the production of hydrazin is favored and yields up to from 70 to 80% of the theoretical amount of hydrazin can be obtained.
- the addition of formaldehyde solution also influences favorably the production of hydrazin, in all robability because of the formation of carbohydrates by the reaction on the formaldehyde of alkali formed during the production of the monochloramin. In all cases an excess of ammonia tends to increase the yield of hydrazin.
- Example 1 Add one (1) liter of sodium hypochlorite solution containing about seventy (70) grams ofactivech lorin to one (1) liter of twenty (20) per cent. ammonia's olution, the temperature being preferably ke t below fifteen (15) degrees centigrade. T e formation of the monochloramin takes place very rapidly and the mixture obtained con-' tains no trace of hypochlorite, but only chloramin and an excess of ammonia. The mixture should without delay be heated to the boiling ⁇ point, whereupon a reaction according to t e equation takes place side by side with the formation of nitrogen.
- Hydrazin is formed and can easily be isolated in the form of the very difficultly soluble sulfate by boiling away the excess of ammonia, acidifying with sulfuric acid, and evaporating till crystallization commences. From twenty-five (25), to thirty (30), grams of hydrazin sulfate, that is, from twenty (20), to t'wenty-five( 25), per cent. of the theoretical yield, are obtained.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
UNITED STATES PATENT OFFICE.
FRIEDRICH RASOHIG, OF LUDWIGSHAFEN-ON-THE-RHINE, GERMANY,
PRODUCTION OF HYDRAZIN.
Specification of Letters Patent.
Patented If an. v26, 1909,
Application filed October 31, 1907. Serial No. 400,002.
To all whom it may concern:
Be it known that I, FRIEDRICH RAsoHIG, doctor of philosophy and chemist, subject of the King of Bavaria, residing at Ludwigshafen on the Rhine, Germany, have invented new and useful Improvements in the.
' suggested that during this reaction a prodnot, monochloramin NH Cl, containing one molecule less water, is formed (Proc. Chem. Soc. 1890, p. 24). It can easily -be proved that this suggestion is correct, for a solution of sodium hypochlorite to which ammonia has been added no longer shows the general reaction of hypochlorites of imparting a violet coloration to anilin-water. It therefore no longer contains hypochlorous acid and actually by distillation in cacao a compound of the composition NH Cl can be isolated in the form of a very volatile oil which is easily soluble in water and possesses a disagreeable odor of chlorid of nitrogen.
I have now discovered that monochloramin can by treatment with ammonia be made to form hydrazin according to the equation NH,01+ NH, NHZNHZIICI.
In order to pre are hydrazin with advantage according to t 's reaction, it is unnecessary and, indeed, inadvisable to isolate the extremely decomposable and oisonou s r nonochloramin and subsequent y treat it with ammonia, but I prefer to treat a hypochlorite directly with an excess of ammonia. The formation of monochloramin takes place practically at once and subsequently two reactions tend to take place of which the first is re resented by the equation given above and feads to the formation of hydrazin, while the second reaction leads to the formation of ammonium chlorid and the liberation of free nitrogen according to the equation Ihave discovered that the second and-undesirable reaction tends to preponderate 1f the mixture of the monochloramin with excess of ammonia be allowed to stand in the cold, or if a catalyser such for instance as small quantities of iron and copper, or a compound such as acetone which lowers-the viscosity of the solution be present. On the other hand, if the mixture containing the monochloramin and ammonia is heated without delay, preferably to the boiling point, or if, either When hot, or when cold, a com ound which increases the viscosity, of the so ution such for instance, as glycerin, sugar, starch, casein, albumen, gum, and glue, is present, the first reaction resulting in the production of hydrazin is favored and yields up to from 70 to 80% of the theoretical amount of hydrazin can be obtained. The addition of formaldehyde solution also influences favorably the production of hydrazin, in all robability because of the formation of carbohydrates by the reaction on the formaldehyde of alkali formed during the production of the monochloramin. In all cases an excess of ammonia tends to increase the yield of hydrazin.
The following examples will serve to illustrate further the nature of my invention and the method'of carrying it into practical effect, but my invention is not confined to these examples.
Example 1. Add one (1) liter of sodium hypochlorite solution containing about seventy (70) grams ofactivech lorin to one (1) liter of twenty (20) per cent. ammonia's olution, the temperature being preferably ke t below fifteen (15) degrees centigrade. T e formation of the monochloramin takes place very rapidly and the mixture obtained con-' tains no trace of hypochlorite, but only chloramin and an excess of ammonia. The mixture should without delay be heated to the boiling }point, whereupon a reaction according to t e equation takes place side by side with the formation of nitrogen. Hydrazin is formed and can easily be isolated in the form of the very difficultly soluble sulfate by boiling away the excess of ammonia, acidifying with sulfuric acid, and evaporating till crystallization commences. From twenty-five (25), to thirty (30), grams of hydrazin sulfate, that is, from twenty (20), to t'wenty-five( 25), per cent. of the theoretical yield, are obtained.
- the boiling Example 2. Stir together three hundred (300) grams of bleaching powder with one (1) liter of twenty (20) per cent. ammonia solution and then rapidly heat the mixture to oint, whereupon considerable quantities o hydrazin are formed. In this case also it can be isolated in the form of hydrazin sulfate by'boiling off the excess of ammonia, acidifying with sulfuric acid, filtering ofl the calcium sulfate formed and evaporatin till crystallization commences.
xample 3; Add twelve (12) cubic centimeters of a five (5) per cent. glue solution to three (3) liters of twenty (20) per cent. ammonia solution, then add further one (1) liter of sodium hypochlorite solution containing about seventy (70) grams of active chlorin, 'and then heat up the mixture finally driving off the excess of ammonia. The residue contains hydrazin which can be conveniently isolated by evaporating the residue and precipitating the hydrazin in the form of its sulfate.
Now what I claim is:
1. The process of producinghydrazin by reacting on monochloramin with ammonia.
2. The process of producing hydrazin by heating monochloramin with an excess of ammonia.
3. The process of producing hydrazin by reacting on monochloramin with ammonia in the presence of a com ound which increases the Viscosity of the so ution.
4. The process of producing hydrazin by reacting on monochloramin with ammonia in the presence of glue.
5. The process of producing hydrazin by heating monochloramin with an excess'of ammonia in the presence of glue.
In testimony whereof I have hereunto set my hand 1n the presence of two subscribing witnesses.
FRIEDRICH RASCHIG. Witnesses:
ERNEST F. EHRHARDT, Jos. H. LEUTE.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US40000207A US910858A (en) | 1907-10-31 | 1907-10-31 | Production of hydrazin. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US40000207A US910858A (en) | 1907-10-31 | 1907-10-31 | Production of hydrazin. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US910858A true US910858A (en) | 1909-01-26 |
Family
ID=2979296
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US40000207A Expired - Lifetime US910858A (en) | 1907-10-31 | 1907-10-31 | Production of hydrazin. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US910858A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2675301A (en) * | 1950-10-23 | 1954-04-13 | Kellogg M W Co | Production of hydrazine |
| US2698286A (en) * | 1949-05-31 | 1954-12-28 | Battelle Development Corp | Dehydration of hydrazine solutions |
| US2710248A (en) * | 1950-01-17 | 1955-06-07 | Univ Ohio State Res Found | Process of forming hydrazine |
| US2784057A (en) * | 1952-10-15 | 1957-03-05 | Exxon Research Engineering Co | Process for treating spent hypochlorite solutions |
| US2785052A (en) * | 1951-06-22 | 1957-03-12 | Metalectro Corp | Production of hydrazine |
| US2837409A (en) * | 1954-03-10 | 1958-06-03 | Univ Ohio State Res Found | Chloramine process |
| US2863728A (en) * | 1955-10-17 | 1958-12-09 | Univ Ohio State Res Found | Production of hydrazine |
| US2917369A (en) * | 1951-06-22 | 1959-12-15 | Nat Distillers Chem Corp | Production of hydrazine |
| US3034861A (en) * | 1959-06-26 | 1962-05-15 | John A Pursley | Process for preparing hydrazine |
| JP2020513385A (en) * | 2016-11-22 | 2020-05-14 | シェフラー テクノロジーズ アー・ゲー ウント コー. カー・ゲーSchaeffler Technologies AG & Co. KG | Method for storing energy in the form of hydrazine carbonate |
-
1907
- 1907-10-31 US US40000207A patent/US910858A/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2698286A (en) * | 1949-05-31 | 1954-12-28 | Battelle Development Corp | Dehydration of hydrazine solutions |
| US2710248A (en) * | 1950-01-17 | 1955-06-07 | Univ Ohio State Res Found | Process of forming hydrazine |
| US2675301A (en) * | 1950-10-23 | 1954-04-13 | Kellogg M W Co | Production of hydrazine |
| US2785052A (en) * | 1951-06-22 | 1957-03-12 | Metalectro Corp | Production of hydrazine |
| US2917369A (en) * | 1951-06-22 | 1959-12-15 | Nat Distillers Chem Corp | Production of hydrazine |
| US2784057A (en) * | 1952-10-15 | 1957-03-05 | Exxon Research Engineering Co | Process for treating spent hypochlorite solutions |
| US2837409A (en) * | 1954-03-10 | 1958-06-03 | Univ Ohio State Res Found | Chloramine process |
| US2863728A (en) * | 1955-10-17 | 1958-12-09 | Univ Ohio State Res Found | Production of hydrazine |
| US3034861A (en) * | 1959-06-26 | 1962-05-15 | John A Pursley | Process for preparing hydrazine |
| JP2020513385A (en) * | 2016-11-22 | 2020-05-14 | シェフラー テクノロジーズ アー・ゲー ウント コー. カー・ゲーSchaeffler Technologies AG & Co. KG | Method for storing energy in the form of hydrazine carbonate |
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